JPS5913632A - Manufacture of beta-manganese dioxide - Google Patents
Manufacture of beta-manganese dioxideInfo
- Publication number
- JPS5913632A JPS5913632A JP57122882A JP12288282A JPS5913632A JP S5913632 A JPS5913632 A JP S5913632A JP 57122882 A JP57122882 A JP 57122882A JP 12288282 A JP12288282 A JP 12288282A JP S5913632 A JPS5913632 A JP S5913632A
- Authority
- JP
- Japan
- Prior art keywords
- manganese dioxide
- mno2
- manganese
- beta
- manufacture
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
【発明の詳細な説明】
本発明はr二酸化マンガンからβ二酸化マンガンを製造
する方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing β-manganese dioxide from r-manganese dioxide.
従来、r二酸化マンガンからβ二酸化マンガンを#造す
る方法としては、β二酸化マンガンを空気中で350℃
〜450Cで加熱しr→β転移させる方法が知られてい
る。しかしこの方法で製造したβ二酸化マンガンをLi
−Mnf(を池の正極活物質として用いても残り結合水
の関係上長時間の安定した放電重圧を得ることはできな
かった。Conventionally, as a method for producing β-manganese dioxide from r-manganese dioxide, β-manganese dioxide was heated in air at 350°C.
A method of heating at ~450C to effect r→β transition is known. However, the β-manganese dioxide produced by this method is
Even if Mnf (-Mnf) was used as the positive electrode active material in the pond, it was not possible to obtain a stable discharge pressure for a long period of time due to the remaining bound water.
また、他の製造方法として(r↓、二価のマンガンイオ
ンを含む酸性溶液中にr二酸化マンガンをスラリーにし
て加温する方法が知られている。この方法には更に静的
方法と動的方法の二つがある。In addition, as another production method (r↓, a method is known in which rmanganese dioxide is slurried in an acidic solution containing divalent manganese ions and heated.This method further includes a static method and a dynamic method. There are two methods.
静的方法とはスラリーで静置した状態で加温処理する方
法であり、動的方法とはスラリーをインペラー攪拌しな
がら加温処理する方法である。The static method is a method in which the slurry is heated while being left still, and the dynamic method is a method in which the slurry is heated while being stirred by an impeller.
しかし、静的方法において1・」2、マンガンイオンが
希薄な場合には転移現象が緩慢でありマンガンイオンが
濃厚な鴨合には生成物は塊状となったり容器に固層した
りして洗滌や取出しが困難になる。一方動的方法では泥
状の生成物となるが、大きくカナバリ合剤成型の時に充
填性に問題が生じる、
本発明は従来知られているγ二゛酸化マンガンからβ二
酸化マンガンを製造する方法のこのような欠点を改良す
る目的でなされたものであり、本発明の方法は二価又は
三11]11のマンガンイオンを含む酸性溶液中にrZ
酸化マンガンをスラリーにして加温するβ二酸化マンガ
ンの刺潰方法に、おいて、当該酸性溶液中にマグネ/ラ
ムイオンを共存せしめたことを特徴と4〜るβ二酸化マ
ンカンの製今方法である。However, in the static method, the transition phenomenon is slow when the manganese ions are dilute, and when the manganese ions are concentrated, the product becomes lumps or forms a solid layer in the container and is difficult to wash. or it becomes difficult to remove. On the other hand, the dynamic method produces a slurry-like product, which causes problems in filling properties when molding the Canabari mixture. The method of the present invention was made to improve such drawbacks, and the method of the present invention involves adding rZ to an acidic solution containing divalent or trivalent manganese ions.
A method for making β-manganese dioxide is characterized in that in the method of crushing β-manganese dioxide in which manganese oxide is made into a slurry and heated, magne/lamb ions are allowed to coexist in the acidic solution.
マンガンイオン儂)(として代、5〜40f/lが)1
r↓濱用いらtしる。Manganese ions (5 to 40 f/l) 1
r↓Hama et al.
酸1<I+温溶液して11よ、イ伍市溶(仮、′等が用
いら第1その+/(ケ10二とじでぐA、50〜52o
q/lが通常用いられろ。Acid 1
q/l is usually used.
マグネシウムイオンの濃度は20〜559/lであ乙。The concentration of magnesium ions is 20 to 559/l.
好斗しくは30〜409/lであイ、。20 y /
を以下ではβ転移現象が緩1炒であり、559/を以上
では硫酸マグネンウJ、が晶出4−.4. 。Preferably 30 to 409/l. 20y/
Below, the β-transition phenomenon is slow, and above 559/, magnenosulfate J crystallizes. 4. .
斗だ2酸n=マンカンのTlj腑紗をそのままマグネン
ウl、イオンの共存する、二価゛マンガンイj7ケ含む
酸性溶級として使用できる。Tlj gauze of dodic acid n = mankan can be used as it is as an acidic solution containing divalent manganese in which magneurium and ions coexist.
”’1+”、マグネシウムイオンの効果は二価のマンガ
ンイオン横変に左右されマンガンイオン濃IWが低い場
合特に有効である。"'1+" The effect of magnesium ions is influenced by the lateral change of divalent manganese ions and is particularly effective when the manganese ion concentration IW is low.
実施例
硫酸、硫酸マグネシウム、r二酸化マンカンを使い硫酸
濃1規110&/V、マグ不ノウムイオンaW35y/
l、二価のマンガンイオン濃度52/lの@液を作製す
る。その溶液300工に粉状のγ二酸化マンガン300
1をスラリー状として90℃力111晶を続けた。Example Using sulfuric acid, magnesium sulfate, r mankan dioxide, concentrated sulfuric acid 1N 110&/V, magnonium ion aW35y/
A @ solution with a divalent manganese ion concentration of 52/l is prepared. Add 300 g of the solution to 300 g of powdered γ manganese dioxide.
1 was made into a slurry and crystallization was continued at 90°C.
120 ■■で塊状物や容器への固着のない沈降性のよ
いに味を帯びた黒色の生成吻を得た。At 120 ■■, a black product with good sedimentation properties without lumps or sticking to the container was obtained.
生成物を300C11Sの(黒水で5回デカンテーショ
ン濾別しケーキを107℃で2H乾燥後、生成物のX線
回折結果はβ二1毀化マンガンであった。二価のマンガ
ンイオン、硫酸a度、マグネシウムイオン、攪拌などの
諸冴因がγ→β転移所要時間、生成β二酸化マンガンの
性状ならびに7時性に与える影響を一括して示す。The product was filtered by decantation using 300C11S (black water) five times, and the cake was dried at 107°C for 2 hours. The effects of various factors such as a degree, magnesium ions, and stirring on the time required for γ→β transition, the properties of the produced β manganese dioxide, and the heptachronicity are shown in one place.
応用例1゜
第一図は、本発明の実り’i!j例■で製造したβ二酸
化マンガンを正極活物質として、導電機に炭素粉末と結
着剤のデフ1コン粉末とで混合成型し電解液にはプロピ
レンカーボネートと162ジメトキ7エタンの混合溶媒
に過塩素酸リチウムをl mo I / /l′/)濃
1ずで溶解し、リチウムマンガン電池を作成したつ結果
は第一図に示すように本発明によるβ二酸化マンガンを
使用した電池い)は長時間安定した放市、′屯圧を示し
イ疋来の加熱法で得たβ二酸化マンガン(B)にみられ
ない優れた特性を有]7ている。Application example 1゜The first figure shows the fruits of the present invention! The β-manganese dioxide produced in Example ① was used as the positive electrode active material, and the conductor was mixed and molded with carbon powder and Def1con powder as a binder, and the electrolyte was mixed with a mixed solvent of propylene carbonate and 162 dimethoxy7 ethane. A lithium manganese battery was prepared by dissolving lithium chlorate at a concentration of l mo I / /l'/). It exhibits stable release and pressure over time, and has excellent properties not seen in β-manganese dioxide (B) obtained by the conventional heating method.
第一図は、本発明の実施例1で得たβ二酸化マンガンを
正極活物質とし/こリチウムマンガン電池、と従来から
リチウムマンガン電池に使用されている1100℃で加
熱処理したβ二酸化マンガンを使用した、リチウムマン
ガン電池の放電曲線を比l′1ツしだものである。Figure 1 shows a lithium-manganese battery using β-manganese dioxide obtained in Example 1 of the present invention as a positive electrode active material, and β-manganese dioxide heat-treated at 1100°C, which is conventionally used in lithium-manganese batteries. This is a comparison of the discharge curve of a lithium manganese battery.
Claims (1)
ガンをスラリーにして加温するβ二酸化マンガンの製造
方法において、当該酸性溶液中に20〜55 y/lの
マグネシウムイオンを共存せしめたことを特徴とするβ
二酸化マンガンの製造方法。A method for producing β-manganese dioxide in which β-manganese dioxide is slurried in an acidic solution containing divalent manganese ions and heated, characterized in that 20 to 55 y/l of magnesium ions are allowed to coexist in the acidic solution. β
Method for producing manganese dioxide.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57122882A JPS5913632A (en) | 1982-07-16 | 1982-07-16 | Manufacture of beta-manganese dioxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57122882A JPS5913632A (en) | 1982-07-16 | 1982-07-16 | Manufacture of beta-manganese dioxide |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5913632A true JPS5913632A (en) | 1984-01-24 |
JPH0239453B2 JPH0239453B2 (en) | 1990-09-05 |
Family
ID=14846966
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57122882A Granted JPS5913632A (en) | 1982-07-16 | 1982-07-16 | Manufacture of beta-manganese dioxide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5913632A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01234330A (en) * | 1988-03-16 | 1989-09-19 | Mitsui Mining & Smelting Co Ltd | Manganese dioxide and its production |
JPH01234331A (en) * | 1988-03-16 | 1989-09-19 | Mitsui Mining & Smelting Co Ltd | Manganic oxide and its production |
JPH0380121A (en) * | 1989-08-22 | 1991-04-04 | Mitsui Mining & Smelting Co Ltd | Production of manganese dioxide for lithium secondary cell |
JPH0380120A (en) * | 1989-08-22 | 1991-04-04 | Mitsui Mining & Smelting Co Ltd | Production of manganese dioxide for lithium primary cell |
JPH0335189U (en) * | 1989-08-14 | 1991-04-05 |
-
1982
- 1982-07-16 JP JP57122882A patent/JPS5913632A/en active Granted
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01234330A (en) * | 1988-03-16 | 1989-09-19 | Mitsui Mining & Smelting Co Ltd | Manganese dioxide and its production |
JPH01234331A (en) * | 1988-03-16 | 1989-09-19 | Mitsui Mining & Smelting Co Ltd | Manganic oxide and its production |
JPH0335189U (en) * | 1989-08-14 | 1991-04-05 | ||
JPH0380121A (en) * | 1989-08-22 | 1991-04-04 | Mitsui Mining & Smelting Co Ltd | Production of manganese dioxide for lithium secondary cell |
JPH0380120A (en) * | 1989-08-22 | 1991-04-04 | Mitsui Mining & Smelting Co Ltd | Production of manganese dioxide for lithium primary cell |
Also Published As
Publication number | Publication date |
---|---|
JPH0239453B2 (en) | 1990-09-05 |
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